US10794250B2 - Electrochemical reactor and internal combustion engine provided with electrochemical reactor - Google Patents

Electrochemical reactor and internal combustion engine provided with electrochemical reactor Download PDF

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US10794250B2
US10794250B2 US16/215,705 US201816215705A US10794250B2 US 10794250 B2 US10794250 B2 US 10794250B2 US 201816215705 A US201816215705 A US 201816215705A US 10794250 B2 US10794250 B2 US 10794250B2
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air
anode layer
water molecules
internal combustion
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US20190195105A1 (en
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Tetsuya Sakuma
Keishi Takada
Hiromasa Nishioka
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Toyota Motor Corp
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Toyota Motor Corp
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    • C—CHEMISTRY; METALLURGY
    • C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
    • C25B15/00—Operating or servicing cells
    • C25B15/02—Process control or regulation
    • C25B15/023—Measuring, analysing or testing during electrolytic production
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/32—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by electrical effects other than those provided for in group B01D61/00
    • B01D53/326—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by electrical effects other than those provided for in group B01D61/00 in electrochemical cells
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/34—Chemical or biological purification of waste gases
    • B01D53/46—Removing components of defined structure
    • B01D53/54—Nitrogen compounds
    • B01D53/56—Nitrogen oxides
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/34—Chemical or biological purification of waste gases
    • B01D53/92—Chemical or biological purification of waste gases of engine exhaust gases
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/34—Chemical or biological purification of waste gases
    • B01D53/92—Chemical or biological purification of waste gases of engine exhaust gases
    • B01D53/94—Chemical or biological purification of waste gases of engine exhaust gases by catalytic processes
    • B01D53/9404—Removing only nitrogen compounds
    • B01D53/9409—Nitrogen oxides
    • B01D53/9431—Processes characterised by a specific device
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/34—Chemical or biological purification of waste gases
    • B01D53/92—Chemical or biological purification of waste gases of engine exhaust gases
    • B01D53/94—Chemical or biological purification of waste gases of engine exhaust gases by catalytic processes
    • B01D53/9495—Controlling the catalytic process
    • C—CHEMISTRY; METALLURGY
    • C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
    • C25B1/00—Electrolytic production of inorganic compounds or non-metals
    • C25B1/01—Products
    • C25B1/02—Hydrogen or oxygen
    • C25B1/04—Hydrogen or oxygen by electrolysis of water
    • C—CHEMISTRY; METALLURGY
    • C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
    • C25B13/00—Diaphragms; Spacing elements
    • C25B13/04—Diaphragms; Spacing elements characterised by the material
    • C—CHEMISTRY; METALLURGY
    • C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
    • C25B9/00—Cells or assemblies of cells; Constructional parts of cells; Assemblies of constructional parts, e.g. electrode-diaphragm assemblies; Process-related cell features
    • C25B9/17—Cells comprising dimensionally-stable non-movable electrodes; Assemblies of constructional parts thereof
    • C25B9/19—Cells comprising dimensionally-stable non-movable electrodes; Assemblies of constructional parts thereof with diaphragms
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01N—GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL COMBUSTION ENGINES
    • F01N3/00—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust
    • F01N3/08—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous
    • F01N3/0892—Electric or magnetic treatment, e.g. dissociation of noxious components
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01N—GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL COMBUSTION ENGINES
    • F01N9/00—Electrical control of exhaust gas treating apparatus
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F02—COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
    • F02D—CONTROLLING COMBUSTION ENGINES
    • F02D41/00—Electrical control of supply of combustible mixture or its constituents
    • F02D41/02—Circuit arrangements for generating control signals
    • F02D41/04—Introducing corrections for particular operating conditions
    • F02D41/12—Introducing corrections for particular operating conditions for deceleration
    • F02D41/123—Introducing corrections for particular operating conditions for deceleration the fuel injection being cut-off
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F02—COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
    • F02D—CONTROLLING COMBUSTION ENGINES
    • F02D41/00—Electrical control of supply of combustible mixture or its constituents
    • F02D41/02—Circuit arrangements for generating control signals
    • F02D41/14—Introducing closed-loop corrections
    • F02D41/1438—Introducing closed-loop corrections using means for determining characteristics of the combustion gases; Sensors therefor
    • F02D41/1444—Introducing closed-loop corrections using means for determining characteristics of the combustion gases; Sensors therefor characterised by the characteristics of the combustion gases
    • F02D41/1454—Introducing closed-loop corrections using means for determining characteristics of the combustion gases; Sensors therefor characterised by the characteristics of the combustion gases the characteristics being an oxygen content or concentration or the air-fuel ratio
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2255/00—Catalysts
    • B01D2255/80—Type of catalytic reaction
    • B01D2255/806—Electrocatalytic
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2257/00—Components to be removed
    • B01D2257/40—Nitrogen compounds
    • B01D2257/404—Nitrogen oxides other than dinitrogen oxide
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2258/00—Sources of waste gases
    • B01D2258/01—Engine exhaust gases
    • B01D2258/012—Diesel engines and lean burn gasoline engines
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/34—Chemical or biological purification of waste gases
    • B01D53/92—Chemical or biological purification of waste gases of engine exhaust gases
    • B01D53/94—Chemical or biological purification of waste gases of engine exhaust gases by catalytic processes
    • B01D53/9445—Simultaneously removing carbon monoxide, hydrocarbons or nitrogen oxides making use of three-way catalysts [TWC] or four-way-catalysts [FWC]
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01N—GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL COMBUSTION ENGINES
    • F01N2240/00—Combination or association of two or more different exhaust treating devices, or of at least one such device with an auxiliary device, not covered by indexing codes F01N2230/00 or F01N2250/00, one of the devices being
    • F01N2240/34—Combination or association of two or more different exhaust treating devices, or of at least one such device with an auxiliary device, not covered by indexing codes F01N2230/00 or F01N2250/00, one of the devices being an electrolyser
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01N—GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL COMBUSTION ENGINES
    • F01N2570/00—Exhaust treating apparatus eliminating, absorbing or adsorbing specific elements or compounds
    • F01N2570/14—Nitrogen oxides
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01N—GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL COMBUSTION ENGINES
    • F01N2900/00—Details of electrical control or of the monitoring of the exhaust gas treating apparatus
    • F01N2900/06—Parameters used for exhaust control or diagnosing
    • F01N2900/08—Parameters used for exhaust control or diagnosing said parameters being related to the engine
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/30—Hydrogen technology
    • Y02E60/36—Hydrogen production from non-carbon containing sources, e.g. by water electrolysis
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02T—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO TRANSPORTATION
    • Y02T10/00—Road transport of goods or passengers
    • Y02T10/10—Internal combustion engine [ICE] based vehicles
    • Y02T10/12—Improving ICE efficiencies
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02T—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO TRANSPORTATION
    • Y02T10/00—Road transport of goods or passengers
    • Y02T10/10—Internal combustion engine [ICE] based vehicles
    • Y02T10/40—Engine management systems

Definitions

  • the present invention relates to an electrochemical reactor and an internal combustion engine provided with an electrochemical reactor.
  • an electrochemical reactor provided with a proton conductive solid electrolyte layer, an anode layer arranged on a surface of the solid electrolyte layer, and a cathode layer arranged on a surface of the solid electrolyte layer (for example, Japanese Unexamined Patent Publication No. 2006-346624).
  • an electrochemical reactor if electric current flows through the anode layer and the cathode layer, water molecules are broken down on the anode layer whereby protons and oxygen are generated, and the NO X reacts with the protons on the cathode layer whereby nitrogen and water molecules are generated.
  • the electrochemical reactor can be used to remove NO X .
  • the concentration of water molecules in the exhaust gas flowing around the electrochemical reactor (concentration of liquid water and steam) will not be constant, but will change according to the operating state of the internal combustion engine. Therefore, depending on the operating state of the internal combustion engine, the concentration of water molecules in the exhaust gas will become lower and accordingly the water molecules supplied to the anode layer will decrease. If in such a state electrical current flows through the anode layer and the cathode layer to continue to break down the water molecules on the anode layer, the amount of water molecules held at the anode layer will decrease.
  • the amount of water molecules held at the anode layer becomes small and the amount of protons moving from the anode layer to the cathode layer decreases.
  • the amount of NO X reduced and removed decreases. Therefore, the performance of the electrochemical reactor in removing NO X decreases.
  • the present invention was made in consideration of the above technical problem and has as its object to cause a decrease in the protons not contributing to the removal of NO X in the electrochemical reactor to thereby suppress the decrease in performance in removing NO X along with a decrease in the amount of water molecules held at the anode layer.
  • the present invention was made so as to solve the above problem and has as its gist the following.
  • An electrochemical reactor comprising: a proton conductive solid electrolyte layer; an anode layer arranged on the surface of the solid electrolyte layer and able to hold water molecules; a cathode layer arranged on the surface of the solid electrolyte layer; and a current control device controlling a current flowing through the anode layer and the cathode layer,
  • the present invention by decreasing the protons not contributing to the removal of NO X in the electrochemical reactor, it is possible to suppress the decrease in the performance in removal of NO X along with a decrease in the amount of water molecules held at the anode layer.
  • FIG. 1 is a schematic view of the configuration of an internal combustion engine.
  • FIG. 2 is a cross-sectional side view of an electrochemical reactor.
  • FIG. 3 is an enlarged cross-sectional view schematically showing a partition wall of the electrochemical reactor.
  • FIG. 4 is an enlarged cross-sectional view schematically showing a partition wall of the electrochemical reactor.
  • FIGS. 5A and 5B are views schematically showing a reaction occurring around a partition wall when current flows from a power system.
  • FIG. 6 is a view showing a relationship between an air-fuel ratio of an air-fuel mixture supplied into the cylinders and a current flowing through an anode layer and a cathode layer.
  • FIG. 7 is a flow chart showing a control routine of current control performed by a power system.
  • FIG. 1 is a schematic view of the configuration of the internal combustion engine 1 .
  • the internal combustion engine 1 is provided with an engine body 10 , fuel feed system 20 , intake system 30 , exhaust system 40 and control device 50 .
  • the engine body 10 is provided with a cylinder block in which a plurality of cylinders 11 are formed, a cylinder head and a crank case.
  • a piston 14 is arranged in each cylinder 11 , and each cylinder 11 is connected to intake ports and exhaust port.
  • the fuel feed system 20 is provided with fuel injectors 21 , a delivery pipe 22 , fuel feed pipe 23 , fuel pump 24 , and fuel tank 25 .
  • Each fuel injector 31 is arranged in the cylinder head so as to directly inject fuel into each cylinder 11 .
  • the fuel pumped out by the fuel pump 24 is supplied through the fuel feed pipe 23 to the delivery pipe 22 , and then is injected from the fuel injector 21 into the cylinder 11 .
  • the intake system 30 is provided with an intake manifold 31 , intake pipe 32 , air cleaner 33 , compressor 34 of a turbocharger 5 , intercooler 35 , and throttle valve 36 .
  • the intake port of each cylinder 11 is communicated through the intake manifold 31 and the intake pipe 32 with the air cleaner 33 .
  • the intake pipe 43 is provided with the compressor 34 of the exhaust turbocharger 5 for compressing and discharging intake air flowing through the intake pipe 32 , and the intercooler 35 for cooling the air compressed by the compressor 34 .
  • the throttle valve 36 is driven so as to be opened and closed, by a throttle valve drive actuator 37 .
  • the exhaust system 40 is provided with an exhaust manifold 41 , exhaust pipe 42 , turbine 43 of the exhaust turbocharger 5 , and electrochemical reactor 70 .
  • the exhaust port of each cylinder 11 is communicated through the exhaust manifold 51 and the exhaust pipe 52 with the electrochemical reactor 70 .
  • the turbine 43 of the exhaust turbocharger 5 which is driven to rotate by the energy of the exhaust gas, is provided.
  • the exhaust system 40 may be provided with a catalyst, such as a three-way catalyst or NO X storage reduction catalyst, upstream side or downstream side of the electrochemical reactor 70 in the flow direction of the exhaust gas.
  • the control device 50 is provided with an electronic control unit (ECU) 51 and various types of sensors.
  • the ECU 51 is comprised of a digital computer, and is provided with components connected with each other through a bidirectional bus 52 , such as a RAM (random access memory) 53 , ROM (read only memory) 54 , CPU (microprocessor) 55 , input port 56 , and output port 57 .
  • RAM random access memory
  • ROM read only memory
  • CPU microprocessor
  • a flow rate sensor (air-flow meter) 61 is provided for detecting the flow rate of air flowing through the intake pipe 32 .
  • air-fuel ratio sensor is provided for detecting the air-fuel ratio of the exhaust gas flowing into the electrochemical reactor 70 .
  • the vehicle including the intake pipe 32 or the internal combustion engine 1 is provided with a humidity sensor 63 for detecting humidity of the air supplied to each cylinder 11 (or outer air). The outputs of these flow rate sensor 61 , air-fuel ratio sensor 62 , and humidity sensor 63 are connected through corresponding AD converters 58 to the input port 56 .
  • a load sensor 65 generating an output voltage proportional to the amount of depression of an accelerator pedal 64 is connected to the accelerator pedal 64 .
  • the output voltage of the load sensor 65 is input through a corresponding AD converter 58 to the input port 56 .
  • a crank angle sensor 66 generates an output pulse every time the crankshaft of the engine body 10 rotates by for example 10 degrees. This output pulse is input to the input port 56 .
  • the engine speed is calculated from the output pulse.
  • the output port 57 of the ECU 51 is connected through corresponding driver circuits 59 to the actuators controlling the operation of the internal combustion engine 1 .
  • the output port 57 is connected to the fuel injectors 21 , fuel pump 24 and throttle valve drive actuator 37 .
  • the ECU 51 outputs control signals controlling these actuators from the output port 57 to control the operation of the internal combustion engine 1 .
  • the control device 50 performs injection control controlling the amount of fuel injected from each fuel injector 21 based on the engine load and engine speed, etc., input in the above manner.
  • injection control basically, the higher the engine load, the more the injection amount is controlled so that the amount of fuel injected from each fuel injector 21 becomes greater during each cycle.
  • the amount of air supplied to the cylinders 11 will not change that much.
  • the higher the engine load the higher the air-fuel ratio of the air-fuel mixture supplied into the cylinders 11 .
  • control device 50 of the present embodiment performs fuel cut control temporarily stopping the injection of fuel from each fuel injector 21 during operation of the internal combustion engine (that is, during rotation of the crankshaft of the engine body 10 ), for example, when the vehicle in which the internal combustion engine 1 is mounted is decelerating. Specifically, fuel cut control is performed and the injection of fuel from each fuel injector 21 is stopped, for example, when the engine load detected by the load sensor 65 is zero, or less than or equal to a predetermined upper limit value and the engine rotational speed calculated based on the output of the crank angle sensor 66 is equal to or greater than a predetermined lower limit value (for example, 2000 rpm).
  • a predetermined lower limit value for example, 2000 rpm
  • the engine body 10 is not provided with spark plugs, and the internal combustion engine 1 is a compression self-ignition type internal combustion engine.
  • the internal combustion engine 1 may also be a spark ignition type internal combustion engine which ignites the air-fuel mixture by a spark from a spark plug.
  • injection control the injection amount is controlled so that the air-fuel ratio of the air-fuel mixture supplied to the cylinders 11 is the target air-fuel ratio.
  • the target air-fuel ratio is, for example, set so as to change near the stoichiometric air-fuel ratio in accordance with the engine operating state.
  • fuel cut control is similarly performed in a spark ignition type internal combustion engine as well.
  • FIG. 2 is a cross-sectional side view of the electrochemical reactor 70 .
  • the electrochemical reactor 70 is provided with partition walls 71 and passages 72 defined by the partition walls.
  • the partition walls 71 are comprised of a plurality of first partition walls extending in parallel with each other and a plurality of second partition walls extending in parallel with each other and perpendicular to the first partition walls.
  • the passages 72 are defined by these first partition walls and second partition walls, and extend in parallel to each other. Therefore, the electrochemical reactor 70 according to the present embodiment has a honeycomb structure. The exhaust gas flowing into the electrochemical reactor 70 flows through the plurality of passages 72 .
  • FIG. 3 is an enlarged cross-sectional view of a partition wall 71 of the electrochemical reactor 70 .
  • a partition wall 71 of the electrochemical reactor 70 is provided with a solid electrolyte layer 75 , an anode layer 76 arranged on one surface of the solid electrolyte layer 75 , and a cathode layer 77 arranged on the surface of the solid electrolyte layer 75 at the opposite side to the surface at which the anode layer 76 is arranged.
  • the solid electrolyte layer 75 includes a porous solid electrolyte having proton conductivity.
  • a perovskite type metal oxide MM′ 1-x R x O 3- ⁇ M ⁇ Ba, Sr, Ca, M′ ⁇ Ce, Zr, R ⁇ Y, Yb, for example, SrZr x Yb 1-x O 3- ⁇ , SrCeO 3 , BaCeO 3 , CaZrO 3 , SrZrO 3 , etc.
  • a phosphate for example, SiO 2 -P 2 O 5 -based glass, etc.
  • metal doped Sn x In 1-x P 2 O 7 for example, SnP 2 O 7 , etc.
  • the anode layer 76 and the cathode layer 77 both include Pt, Pd, Rh, or other precious metals. Further, the anode layer 76 includes a substance able to hold (that is, able to adsorb and/or absorb) water molecules. Specifically, the substance able to hold water molecules includes zeolite, silica gel, activated alumina, etc. On the other hand, the cathode layer 77 includes a substance able to hold (that is, able to adsorb and/or absorb) NO X . Specifically, the substance able to hold NO X includes K, Na, or another alkali metal, Ba or another alkali earth metal, La or another rare earth, etc.
  • the electrochemical reactor 70 is provided with a power system 73 and ammeter 74 .
  • the positive electrode of the power system 73 is connected to the anode layer 76
  • the negative electrode of the power system 73 is connected to the cathode layer 77 .
  • the power system 73 is configured to be able to change the current flowing through the cathode layer 77 , solid electrolyte layer 75 , and anode layer 76 .
  • the power system 73 is configured to be able to change the voltage applied across the anode layer 76 and the cathode layer 77 .
  • the power system 73 is connected to the ammeter 74 in series. Further, the ammeter 74 is connected through a corresponding AD converter 58 to the input port 56 . The power system 73 is connected through a corresponding drive circuit 59 to the output port 57 of the ECU 51 . The power system 73 is controlled by the ECU 51 . Therefore, the power system 73 and ECU 51 function as a current control device for controlling the current flowing through the anode layer 76 and the cathode layer 77 . In particular, in the present embodiment, the power system 73 is controlled so that the current value detected by the ammeter 74 becomes a target value.
  • the water molecules held at the anode layer 76 are electrolyzed whereby oxygen and protons are generated.
  • the generated oxygen is released into the exhaust gas, while the generated protons move from the anode layer 76 through the the solid electrolyte layer 75 to the cathode layer 77 .
  • the NO held at the cathode layer 77 reacts with the protons and electrons whereby nitrogen and water molecules are generated.
  • the anode layer 76 and the cathode layer 77 are arranged on two surfaces at the opposite sides of the solid electrolyte layer 75 .
  • the anode layer 76 and the cathode layer 77 may also be arranged on the same surface of the solid electrolyte layer 75 . In this case, the protons move through the vicinity of the surface of the solid electrolyte layer 75 at which the anode layer 76 and the cathode layer 77 are arranged.
  • the anode layer 76 may include two layers of a conductive layer 76 a including a precious metal having electroconductivity and a water molecule holding layer 76 b including a substance able to hold water molecules.
  • the conductive layer 76 a is arranged on the surface of the solid electrolyte layer 75
  • the water molecule holding layer 76 b is arranged on the surface of the conductive layer 76 a at the opposite side from the solid electrolyte layer 75 side.
  • the cathode layer 77 may include two layers of a conductive layer 77 a including a precious metal having electroconductivity and an NO X holding layer 77 b including a substance able to hold NO X .
  • the conductive layer 77 a is arranged on the surface of the solid electrolyte layer 75
  • the NO X holding layer 77 b is arranged on the surface of the conductive layer 77 a at the opposite side from the solid electrolyte layer 75 side.
  • FIG. 5A is a view schematically showing the reaction which occurs around a partition wall 71 , when the current flowing from the power system 73 is small.
  • FIG. 5B is a view schematically showing the reaction which occurs around a partition wall 71 , when the current flowing from the power system 73 is large.
  • the concentration of the water molecules included in the exhaust gas changes according to the engine operating state. That is, if the air-fuel mixture burns in the cylinders 11 of the engine body 10 , water molecules are generated along with combustion. Therefore, if the engine operating state changes and the amount of fuel supplied from the fuel injectors 21 changes, the concentration of the water molecules included in the exhaust gas changes. Therefore, for example, when the above-mentioned fuel cut control is being performed, the exhaust gas includes almost no water molecules.
  • the ratio of the air to the supplied fuel is higher. Therefore, at this time, after the air-fuel mixture is burned in the cylinders 11 , the ratio of the air to the water molecules in the exhaust gas is high, and therefore the concentration of water molecules in the exhaust gas is low. Therefore, the concentration of water molecules in the exhaust gas changes according to the air-fuel ratio of the air-fuel mixture supplied into the cylinders 11 .
  • the concentration of water molecules in the exhaust gas is low, the amount of water molecules held at the anode layer 76 in the equilibrium state is small. Therefore, if the concentration of water molecules in the exhaust gas decreases, the amount of water molecules held at the anode layer 76 decreases.
  • the power system 73 makes the current flowing through the anode layer 76 and the cathode layer 77 smaller, when the water molecules held at the anode layer 76 are relatively small in number, compared to when they are relatively great in number.
  • the power system 73 reduces the current flowing through the anode layer 76 and the cathode layer 77 , as the water molecules held at the anode layer 76 become smaller in amount.
  • FIG. 6 is a view showing the relationship of the air-fuel ratio of the air-fuel mixture supplied into the cylinders 11 and the current flowing through the anode layer 76 and the cathode layer 77 .
  • the concentration of water molecules in the exhaust gas decreases, and as a result the water molecules held at the anode layer 76 tend to decrease. Therefore, in the example shown in FIG. 6 , as the air-fuel ratio of the air-fuel mixture supplied into the cylinders 11 becomes higher, that is, as the water molecules held at the anode layer 76 become fewer, the current flowing through the anode layer 76 and the cathode layer 77 is made smaller. Note that, in the example shown in FIG. 6 , the current is made smaller in proportion to the air-fuel ratio of the air-fuel mixture becoming higher, but it is not necessarily required to change the current proportionally to the air-fuel ratio of the air-fuel mixture.
  • the power system 73 makes the current flowing through the anode layer 76 and the cathode layer 77 extremely small, when air is supplied without fuel being supplied into the cylinders 11 due to fuel cut control.
  • the power system 73 makes the current flowing through the anode layer 76 and the cathode layer 77 at this time substantially zero.
  • the power system 73 can be said to change the current flowing through the anode layer 76 and the cathode layer 77 to become smaller, when the water molecules held at the anode layer 76 change to become smaller in amount.
  • the time when the water molecules held at the anode layer 76 become smaller in amount means the time when the concentration of water molecules in the exhaust gas has decreased. Further, the time when the water molecules held at the anode layer 76 become smaller in amount, includes not only the time when the water molecules held at the anode layer 76 actually change to become smaller in amount, but also the time when the water molecules held at the anode layer 76 are expected to become smaller in amount due to various actuators (fuel injectors 21 , throttle valve 36 , etc.) of the internal combustion engine 1 being operated.
  • various actuators fuel injectors 21 , throttle valve 36 , etc.
  • the time when the water molecules held at the anode layer 76 become smaller in amount includes, for example, the time when the air-fuel ratio of the air-fuel mixture supplied to the cylinders 11 changes (to the lean side) to become higher or the time when fuel cut control is started.
  • FIG. 7 is a flow chart showing a control routine of current control performed by the power system 73 .
  • the illustrated control routine is performed every certain time interval.
  • step S 11 the amount of fuel injection Q from each fuel injector 21 to a cylinder 11 in each cycle is acquired.
  • the amount of fuel injection Q is, for example, calculated based on the target amount of fuel injection from each fuel injector 21 calculated at the ECU 51 .
  • Each fuel injector 21 is controlled so that the amount of fuel injection from the fuel injector 21 at each cycle becomes the target amount of fuel injection.
  • step S 12 it is judged if the amount of fuel injection Q to each cylinder 11 acquired at step S 11 is greater than 0. If, at step S 12 , it is judged that the amount of fuel injection Q to each cylinder 11 is greater than 0, that is, if it is judged that fuel cut control is not underway, the routine proceeds to step S 13 .
  • step S 13 using the air-fuel ratio sensor 62 , the air-fuel ratio of the exhaust gas flowing into the electrochemical reactor 70 is acquired.
  • step S 14 the target current value I is calculated using a map such as shown in FIG. 6 , based on the air-fuel ratio of the exhaust gas acquired at step S 13 .
  • the power system 73 is controlled so that the current flowing through the anode layer 76 and the cathode layer 77 becomes the target current value I, then the control routine is ended.
  • step S 12 determines whether the amount of fuel injection Q to each cylinder 11 is 0 or not. If it is judged that a fuel cut is underway, the routine proceeds to step S 15 .
  • the target current value I is set to zero. Therefore, the power system 73 is controlled so as not to make electrical current flow through the anode layer 76 and the cathode layer 77 , then the control routine is ended.
  • the concentration of water molecules in the exhaust gas is low, that is, when the water molecules held at the anode layer 76 are relatively small in number, the current flowing through the anode layer 76 and the cathode layer 77 is made smaller. Due to this, it is suppressed to generate excessive protons, it can be suppressed to decrease the amount of the water molecules held at the anode layer 76 , and decrease in the NO X removal performance accompanying a decrease in the amount of the water molecules held at the anode layer 76 , can be suppressed.
  • reaction speed “v” in the reaction of NO X and the protons held in the cathode layer 77 is expressed by the following formula (1):
  • A, ⁇ , and ⁇ are constants, ⁇ E indicates the activating energy, R indicates the gas constant, and T indicates the temperature. Further, [NO X ] indicates the concentration of NO X , while [H + ] indicates the concentration of protons.
  • the reaction speed “v” in the reaction between NO X and the protons becomes faster as the concentration [NO X ] of NO X becomes higher and as the concentration [H + ] of protons becomes higher.
  • the air-fuel ratio of the exhaust gas is the rich air-fuel ratio
  • the NO X in the exhaust gas reacts with the unburned HC, CO, etc. in the exhaust gas, and therefore the concentration of the NO X in the exhaust gas is low. Therefore, in this case, the amount of NO X held at the cathode layer 77 tends to decrease. If the amount of NO X held at the cathode layer 77 decreases in this way, the concentration [NO X ] of NO X in the formula (1) decreases, and therefore the reaction speed in the reaction of NO X and protons becomes slower.
  • the higher the air-fuel ratio of the air-fuel mixture supplied to each cylinder 11 the smaller the current flowing through the anode layer 76 and the cathode layer 77 .
  • the lower the air-fuel ratio of the exhaust gas the more to the rich side the air-fuel ratio
  • the more the amount of protons supplied to the cathode layer 77 per unit time is increased.
  • the concentration [H+] of protons in the formula (1) increases. Therefore, according to the present embodiment, even when the air-fuel ratio of the exhaust gas is the rich air-fuel ratio, the reaction speed in the reaction between NO X and the protons can be maintained high.
  • the current flowing through the anode layer 76 and the cathode layer 77 was controlled in accordance with the air-fuel ratio of the air-fuel mixture supplied into the cylinders 11 and whether or not fuel cut control is performed.
  • the amount of the water molecules held at the anode layer 76 also changes according to other factors.
  • the power system 73 may be controlled so that as the temperature of the electrochemical reactor 70 becomes higher, the current flowing through the anode layer 76 and the cathode layer 77 is made smaller.
  • the power system 73 may be controlled so as to make the current flowing through the anode layer 76 and the cathode layer 77 smaller, as the humidity detected by the humidity sensor 63 becomes lower.
  • the power system 73 is controlled so that the current flowing through the anode layer 76 and the cathode layer 77 is zero, during execution of fuel cut control.
  • the power system 73 may also be controlled so that current slightly flows through the anode layer 76 and the cathode layer 77 , even during execution of fuel cut control.
  • the concentration of water molecules in the gas flowing into the electrochemical reactor 70 changes in accordance with the humidity of the air supplied to the cylinders 11 , and therefore preferably the current flowing through the anode layer 76 and the cathode layer 77 is made smaller, as the humidity detected by the humidity sensor 63 becomes lower.

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US11358095B2 (en) 2019-01-08 2022-06-14 Toyota Jidosha Kabushiki Kaisha Electrochemical reactor

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JP2023180376A (ja) * 2022-06-09 2023-12-21 トヨタ自動車株式会社 内燃機関の排気浄化装置

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US11358095B2 (en) 2019-01-08 2022-06-14 Toyota Jidosha Kabushiki Kaisha Electrochemical reactor

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US20190195105A1 (en) 2019-06-27
CN109958511A (zh) 2019-07-02
JP6881279B2 (ja) 2021-06-02
JP2019116841A (ja) 2019-07-18
EP3505730A1 (en) 2019-07-03
KR20190078511A (ko) 2019-07-04
RU2702070C1 (ru) 2019-10-03
BR102018076477A2 (pt) 2019-08-20
CN109958511B (zh) 2021-04-23

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